DE579143C - Process for the extraction of sulphates of iron, copper, zinc and nickel - Google Patents

Process for the extraction of sulphates of iron, copper, zinc and nickel

Info

Publication number
DE579143C
DE579143C DEA60862D DEA0060862D DE579143C DE 579143 C DE579143 C DE 579143C DE A60862 D DEA60862 D DE A60862D DE A0060862 D DEA0060862 D DE A0060862D DE 579143 C DE579143 C DE 579143C
Authority
DE
Germany
Prior art keywords
sulphates
iron
zinc
extraction
copper
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
DEA60862D
Other languages
German (de)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GEORG AGDE DR
Original Assignee
GEORG AGDE DR
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from DEA49573D external-priority patent/DE458191C/en
Application filed by GEORG AGDE DR filed Critical GEORG AGDE DR
Priority to DEA60862D priority Critical patent/DE579143C/en
Application granted granted Critical
Publication of DE579143C publication Critical patent/DE579143C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G1/00Methods of preparing compounds of metals not covered by subclasses C01B, C01C, C01D, or C01F, in general
    • C01G1/10Sulfates
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/22Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Description

Verfahren zur Gewinnung von Sulfaten des Eisens, Kupfers, Zinks und Nickels Nach dem Verfahren des Patents 431 581 werden aus Sulfatlösungen, wie sie z: B. als sogenannte Beizlaugen zum Abbeizen von Glühzunder benutzt werden, die Vitriole so gewonnen, daß man der zu kristallisierenden Lösung vor der Abkühlung und Kristallisation so viel konzentrierte Schwefelsäure zusetzt, daß man nach der Kristallisation die von den Kristallen befreite Mutterlauge ohne besonderen Zusatz von Schwefelsäure sofort wieder in wirtschaftlicher Weise zum Lösen von Metallen benutzen kann. Nach dem Verfahren des Patents 458 191 erreicht man dasselbe, wenn man Laugen, die mindestens noch einige Prozente freie Säure enthalten, tief abkühlt.Process for the extraction of sulphates of iron, copper, zinc and Nickels According to the method of patent 431 581, sulfate solutions like them e.g. used as so-called pickling liquors for stripping glowing scale, which Vitriole obtained in such a way that one of the solution to be crystallized before cooling and crystallization so much concentrated sulfuric acid is added that after the Crystallization of the mother liquor freed from the crystals without any special addition of sulfuric acid immediately again in an economical way for dissolving metals can use. According to the method of patent 458 191 the same thing is achieved if alkalis that contain at least a few percent free acid are deeply cooled.

Gemäß der vorliegenden Erfindung kann man nun die gleiche Aufgabe wie im Patent 458 191,, nämlich die Gewinnung von reinen Vitriolen, d. h. solchen, die frei von Sulfaten mit weniger als 7 Mol. Kristallwasser sind, und die gleichzeitige Erzielung einer sofort wieder brauchbaren Lauge, die also vor oder nach der Kristallisation keinen besonderen Schwefelsäurezusatz erhält, auch ohne Tiefkühlung, nämlich bei Durchschnittsaußentemperaturen, erreichen, wenn man von Laugen ausgeht, die neben freier Säure besonders viel Vitriol enthalten, so daß nach der Entfernung der durch Abkühlung auf Durchschnittsaußentemperatur abgeschiedenen Kristalle der Gehalt -an freier Säure in der Mutterlauge so hoch ist, daB ohne vorherigen besonderen Säurezusatz eine wirtschaftliche Wiederverwendung zur Herstellung weiterer Vitriolmengen möglich ist. Solche Laugen sind z. B. 1 roo.g Eisenvitriol/1 und 2o g Schwefelsäure/1 bei einer Temperatur von rund 70° u. a. Dieser Befund ist aus zwei Gründen neu und überraschend. Einmal war es auf Grund der bisher bekannten Unterlagen nicht möglich, vorauszusehen, ob man unter diesen Bedingungen reinen Vitriol - d. h. von Hydraten mit weniger als 7 Mol. Kristallwasser freies Salz - bekommen würde und dann, daB die Mutterlauge ohne besonderen Zusatz von Schwefelsäure wieder eine arbeitskräftige Lauge sein würde. Beispiel Aus einer Beizlauge von 68° Temperatur mit 1 050 g Eisenvitriol und 30 911 freier Säure .wird durch Abkühlen auf 15° eine Mutterlauge erhalten, die 385 g Eisenvitriol/1 und 54 g/1 freie Säure enthält. Der Gehalt an freier Säure ist also das 1,8fache des Gehalts der Ausgangslösung.According to the present invention, the same task as in patent 458 191, namely the production of pure vitriols, ie those which are free from sulfates with less than 7 mol. which does not receive any special addition of sulfuric acid before or after crystallization, even without deep freezing, namely at average outside temperatures, if one starts out from alkalis which, in addition to free acid, contain a particularly large amount of vitriol, so that after the removal of the crystals separated by cooling to average outside temperature the content - of free acid in the mother liquor is so high that is possible without any previous particular acid addition an economical recycling for the production of further Vitriolmengen. Such alkalis are z. B. 1 roo.g iron vitriol / 1 and 20 g sulfuric acid / 1 at a temperature of around 70 °, etc. This finding is new and surprising for two reasons. On the one hand, on the basis of the documents known up to now, it was not possible to foresee whether pure vitriol would be obtained under these conditions - that is, salt free from hydrates with less than 7 mol laborious lye would be. Example From a pickling liquor of 68 ° temperature with 1050 g ferrous sulphate and 30,911 free acid .If obtain a mother liquor by cooling to 15 °, containing 385 g ferrous sulphate / 1 and 54 g / 1 free acid. The content of free acid is therefore 1.8 times the content of the starting solution.

Die Vorteile der Erfindung treten besonders da in Erscheinung und sind von besonderer wirtschaftlicher Wichtigkeit, wo man bei der Vitriolherstellung bzw. beim Abbeizen von. Glühzunder mit relativ geringen Säuregehalten arbeitet, weil bei höheren Säurekonzentrationen eine Reihe technischer Nachteile, z. B. BeizblasenbiUung auf Blechen u. a., entstehen, wo also die sogenannte Auffrischungsspanne,, d. h. die Differenz zwischen den jeweils erlaubten blindest- und Höchstgehalten, an freier Säure verhältnismäßig gering ist.The advantages of the invention are particularly evident there and are of particular economic importance, where to look at vitriol production or when stripping. Annealing scale with a relatively low acid content is working, because at higher acid concentrations a number of technical disadvantages, e.g. B. Pickling bubble formation on sheet metal, among other things, arise, so where the so-called refreshment margin, d. H. the difference between the respectively permitted minimum and maximum levels, in terms of freer Acid is relatively low.

Gegenüber dem Patent 458 igi ist der Vorteil gegeben, daß die Aufwendungen für Erzeugung tiefer Temperaturen, Kälteanlage, deren Kraftbedarf usw. überflüssig werden und die Apparatur wesentlich kleiner, und zwar nur rund halb so groß zu sein braucht.Compared to the patent 458 igi there is the advantage that the expenses for generating low temperatures, refrigeration systems, their power requirements, etc. superfluous and the equipment is much smaller, only about half the size needs.

Claims (1)

PATENTANSPRUCH: Abänderung des Verfahrens zur Gewinnung kristallisierter Sulfate nach Patent 458 igi, dadurch gekennzeichnet, daß man von Ablaugen solcher Sulfat- und Schwefelsäuregehalte ausgeht, daß bei Abkühlung der Laugen auf gewöhnliche Temperatur die Sulfate in Form reinerVitriole sich ausscheiden und näch deren Entfernung eine Mutterlauge zurückbleibt, die unmittelbar wieder als Arbeitsflüssigkeit Verwendung finden kann. PATENT CLAIM: Modification of the process for the production of crystallized sulphates according to Patent 458 igi, characterized in that one starts from liquors with such sulphate and sulfuric acid contents that when the liquors are cooled to the usual temperature, the sulphates precipitate in the form of pure vitriols and a mother liquor remains after their removal that can be used again immediately as working fluid.
DEA60862D 1926-12-23 1931-02-22 Process for the extraction of sulphates of iron, copper, zinc and nickel Expired DE579143C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEA60862D DE579143C (en) 1926-12-23 1931-02-22 Process for the extraction of sulphates of iron, copper, zinc and nickel

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEA49573D DE458191C (en) 1926-12-23 1926-12-23 Process for the production of crystallized sulphates of iron, copper, zinc and nickel
DEA60862D DE579143C (en) 1926-12-23 1931-02-22 Process for the extraction of sulphates of iron, copper, zinc and nickel

Publications (1)

Publication Number Publication Date
DE579143C true DE579143C (en) 1933-06-21

Family

ID=25964200

Family Applications (1)

Application Number Title Priority Date Filing Date
DEA60862D Expired DE579143C (en) 1926-12-23 1931-02-22 Process for the extraction of sulphates of iron, copper, zinc and nickel

Country Status (1)

Country Link
DE (1) DE579143C (en)

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